Mixture of 1-Propanol + Acetonitrile

Datasets

1. Mole fraction (6)
2. ρ_l - Mass density, kg/m3 (4)
3. γ - Surface tension liquid-gas, N/m (4)
4. T_boil - Boiling temperature at pressure P, K (6)

Mole fraction of Acetonitrile (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetonitrile (2) - Liquid	Mole fraction of Acetonitrile (2) - Gas
0.0610	0.2050
0.1110	0.3200
0.1510	0.3910
0.2080	0.4700
0.2530	0.5260
0.3490	0.5940
0.4110	0.6230
0.4650	0.6440
0.5120	0.6620
0.5700	0.6830
0.6290	0.7060
0.6900	0.7310
0.7250	0.7330
0.7800	0.7480
0.8290	0.7750
0.8830	0.8020
0.9460	0.8410
0.9790	0.9020
0.9960	0.9410

Mole fraction of Acetonitrile (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetonitrile (2) - Liquid	Mole fraction of Acetonitrile (2) - Gas
0.0000	0.0000
0.0520	0.1930
0.1030	0.3170
0.1520	0.4020
0.2050	0.4630
0.2460	0.5100
0.3010	0.5460
0.3450	0.5770
0.4020	0.6030
0.4530	0.6260
0.5010	0.6480
0.5520	0.6690
0.5890	0.6910
0.6510	0.7140
0.7030	0.7380
0.7480	0.7650
0.7980	0.7960
0.8530	0.8330
0.9020	0.8710
0.9480	0.9310
1.0000	1.0000

Mole fraction of Acetonitrile (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetonitrile (2) - Liquid	Mole fraction of Acetonitrile (2) - Gas
0.0615	0.2058
0.1121	0.3210
0.1519	0.3916
0.2086	0.4712
0.2539	0.5270
0.2910	0.5576
0.3498	0.5945
0.4115	0.6237
0.4661	0.6454
0.5132	0.6629
0.5707	0.6842
0.6300	0.7072
0.6907	0.7324
0.7235	0.7470
0.7792	0.7739
0.8283	0.8014
0.8824	0.8399
0.9451	0.9010
0.9776	0.9398
0.9953	0.9654

Mole fraction of Acetonitrile (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetonitrile (2) - Liquid	Mole fraction of Acetonitrile (2) - Gas
0.0610	0.2050
0.1110	0.3200
0.1510	0.3910
0.2080	0.4700
0.2530	0.5260
0.3490	0.5940
0.4110	0.6230
0.4650	0.6440
0.5120	0.6620
0.5700	0.6830
0.6290	0.7060
0.6900	0.7310
0.7250	0.7330
0.7800	0.7480
0.8290	0.7750
0.8830	0.8020
0.9460	0.8410
0.9790	0.9020
0.9960	0.9410

Mole fraction of Acetonitrile (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetonitrile (2) - Liquid	Mole fraction of Acetonitrile (2) - Gas
0.0000	0.0000
0.0520	0.1930
0.1030	0.3170
0.1520	0.4020
0.2050	0.4630
0.2460	0.5100
0.3010	0.5460
0.3450	0.5770
0.4020	0.6030
0.4530	0.6260
0.5010	0.6480
0.5520	0.6690
0.5890	0.6910
0.6510	0.7140
0.7030	0.7380
0.7480	0.7650
0.7980	0.7960
0.8530	0.8330
0.9020	0.8710
0.9480	0.9310
1.0000	1.0000

Mole fraction of Acetonitrile (2) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetonitrile (2) - Liquid	Mole fraction of Acetonitrile (2) - Gas
0.0615	0.2058
0.1121	0.3210
0.1519	0.3916
0.2086	0.4712
0.2539	0.5270
0.2910	0.5576
0.3498	0.5945
0.4115	0.6237
0.4661	0.6454
0.5132	0.6629
0.5707	0.6842
0.6300	0.7072
0.6907	0.7324
0.7235	0.7470
0.7792	0.7739
0.8283	0.8014
0.8824	0.8399
0.9451	0.9010
0.9776	0.9398
0.9953	0.9654

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Acetonitrile (2) - Liquid	Mass density, kg/m3 - Liquid
278.15	0.0000	816.3
278.15	0.1255	813.41
278.15	0.2452	810.66
278.15	0.3466	808.33
278.15	0.4995	804.81
278.15	0.6449	801.47
278.15	0.7492	799.07
278.15	0.8645	796.42
278.15	0.9101	795.37
278.15	1.0000	793.3
283.15	0.0000	812.4
283.15	0.1255	809.44
283.15	0.2452	806.61
283.15	0.3466	804.22
283.15	0.4995	800.61
283.15	0.6449	797.18
283.15	0.7492	794.72
283.15	0.8645	792.0
283.15	0.9101	790.92
283.15	1.0000	788.8
288.15	0.0000	808.6
288.15	0.1255	805.55
288.15	0.2452	802.64
288.15	0.3466	800.18
288.15	0.4995	796.46
288.15	0.6449	792.93
288.15	0.7492	790.39
288.15	0.8645	787.59
288.15	0.9101	786.48
288.15	1.0000	784.3
293.15	0.0000	803.61
293.15	0.1255	799.41
293.15	0.2452	796.56
293.15	0.3466	794.15
293.15	0.4995	790.51
293.15	0.6449	787.05
293.15	0.7492	784.57
293.15	0.8645	781.82
293.15	0.9101	780.74
293.15	1.0000	778.3
298.15	0.0000	799.58
298.15	0.1255	796.74
298.15	0.2452	794.01
298.15	0.3466	791.7
298.15	0.4995	788.21
298.15	0.6449	784.9
298.15	0.7492	782.52
298.15	0.8645	779.89
298.15	0.9101	778.85
298.15	1.0000	776.75
303.15	0.0000	795.48
303.15	0.1255	792.49
303.15	0.2452	789.62
303.15	0.3466	787.18
303.15	0.4995	783.51
303.15	0.6449	780.02
303.15	0.7492	777.52
303.15	0.8645	774.75
303.15	0.9101	773.66
303.15	1.0000	771.5
308.15	0.0000	792.8
308.15	0.1255	789.47
308.15	0.2452	786.3
308.15	0.3466	783.62
308.15	0.4995	779.56
308.15	0.6449	775.71
308.15	0.7492	772.95
308.15	0.8645	769.89
308.15	0.9101	768.68
308.15	1.0000	766.3
313.15	0.0000	787.02
313.15	0.1255	783.74
313.15	0.2452	780.62
313.15	0.3466	777.99
313.15	0.4995	774.01
313.15	0.6449	770.23
313.15	0.7492	767.52
313.15	0.8645	764.52
313.15	0.9101	763.34
313.15	1.0000	761.0

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 293.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Acetonitrile (2) - Liquid	Mass density, kg/m3 - Liquid
0.1004	799.54
0.2018	797.63
0.3013	795.62
0.5004	791.05
0.7003	785.97
0.8002	783.29
0.8997	780.68

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Acetonitrile (2) - Liquid	Mass density, kg/m3 - Liquid
278.15	0.0000	816.3
278.15	0.1255	813.41
278.15	0.2452	810.66
278.15	0.3466	808.33
278.15	0.4995	804.81
278.15	0.6449	801.47
278.15	0.7492	799.07
278.15	0.8645	796.42
278.15	0.9101	795.37
278.15	1.0000	793.3
283.15	0.0000	812.4
283.15	0.1255	809.44
283.15	0.2452	806.61
283.15	0.3466	804.22
283.15	0.4995	800.61
283.15	0.6449	797.18
283.15	0.7492	794.72
283.15	0.8645	792.0
283.15	0.9101	790.92
283.15	1.0000	788.8
288.15	0.0000	808.6
288.15	0.1255	805.55
288.15	0.2452	802.64
288.15	0.3466	800.18
288.15	0.4995	796.46
288.15	0.6449	792.93
288.15	0.7492	790.39
288.15	0.8645	787.59
288.15	0.9101	786.48
288.15	1.0000	784.3
293.15	0.0000	803.61
293.15	0.1255	799.41
293.15	0.2452	796.56
293.15	0.3466	794.15
293.15	0.4995	790.51
293.15	0.6449	787.05
293.15	0.7492	784.57
293.15	0.8645	781.82
293.15	0.9101	780.74
293.15	1.0000	778.3
298.15	0.0000	799.58
298.15	0.1255	796.74
298.15	0.2452	794.01
298.15	0.3466	791.7
298.15	0.4995	788.21
298.15	0.6449	784.9
298.15	0.7492	782.52
298.15	0.8645	779.89
298.15	0.9101	778.85
298.15	1.0000	776.75
303.15	0.0000	795.48
303.15	0.1255	792.49
303.15	0.2452	789.62
303.15	0.3466	787.18
303.15	0.4995	783.51
303.15	0.6449	780.02
303.15	0.7492	777.52
303.15	0.8645	774.75
303.15	0.9101	773.66
303.15	1.0000	771.5
308.15	0.0000	792.8
308.15	0.1255	789.47
308.15	0.2452	786.3
308.15	0.3466	783.62
308.15	0.4995	779.56
308.15	0.6449	775.71
308.15	0.7492	772.95
308.15	0.8645	769.89
308.15	0.9101	768.68
308.15	1.0000	766.3
313.15	0.0000	787.02
313.15	0.1255	783.74
313.15	0.2452	780.62
313.15	0.3466	777.99
313.15	0.4995	774.01
313.15	0.6449	770.23
313.15	0.7492	767.52
313.15	0.8645	764.52
313.15	0.9101	763.34
313.15	1.0000	761.0

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 293.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of Acetonitrile (2) - Liquid	Mass density, kg/m3 - Liquid
0.1004	799.54
0.2018	797.63
0.3013	795.62
0.5004	791.05
0.7003	785.97
0.8002	783.29
0.8997	780.68

Surface tension liquid-gas, N/m [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Acetonitrile (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
278.15	0.0000	0.0249
278.15	0.1255	0.0252
278.15	0.2452	0.0254
278.15	0.3466	0.0258
278.15	0.4995	0.0265
278.15	0.6449	0.0274
278.15	0.7492	0.0281
278.15	0.8645	0.0291
278.15	0.9101	0.0295
278.15	1.0000	0.0305
283.15	0.0000	0.0245
283.15	0.1255	0.0248
283.15	0.2452	0.0250
283.15	0.3466	0.0254
283.15	0.4995	0.0261
283.15	0.6449	0.0270
283.15	0.7492	0.0277
283.15	0.8645	0.0287
283.15	0.9101	0.0291
283.15	1.0000	0.0301
288.15	0.0000	0.0241
288.15	0.1255	0.0244
288.15	0.2452	0.0247
288.15	0.3466	0.0250
288.15	0.4995	0.0257
288.15	0.6449	0.0266
288.15	0.7492	0.0273
288.15	0.8645	0.0283
288.15	0.9101	0.0287
288.15	1.0000	0.0297
293.15	0.0000	0.0237
293.15	0.1255	0.0240
293.15	0.2452	0.0243
293.15	0.3466	0.0246
293.15	0.4995	0.0253
293.15	0.6449	0.0262
293.15	0.7492	0.0269
293.15	0.8645	0.0279
293.15	0.9101	0.0283
293.15	1.0000	0.0293
298.15	0.0000	0.0233
298.15	0.1255	0.0236
298.15	0.2452	0.0239
298.15	0.3466	0.0242
298.15	0.4995	0.0249
298.15	0.6449	0.0258
298.15	0.7492	0.0266
298.15	0.8645	0.0275
298.15	0.9101	0.0279
298.15	1.0000	0.0289
303.15	0.0000	0.0229
303.15	0.1255	0.0232
303.15	0.2452	0.0235
303.15	0.3466	0.0238
303.15	0.4995	0.0245
303.15	0.6449	0.0254
303.15	0.7492	0.0262
303.15	0.8645	0.0271
303.15	0.9101	0.0275
303.15	1.0000	0.0285
308.15	0.0000	0.0225
308.15	0.1255	0.0228
308.15	0.2452	0.0231
308.15	0.3466	0.0234
308.15	0.4995	0.0242
308.15	0.6449	0.0250
308.15	0.7492	0.0258
308.15	0.8645	0.0267
308.15	0.9101	0.0271
308.15	1.0000	0.0281
313.15	0.0000	0.0222
313.15	0.1255	0.0224
313.15	0.2452	0.0227
313.15	0.3466	0.0230
313.15	0.4995	0.0238
313.15	0.6449	0.0246
313.15	0.7492	0.0254
313.15	0.8645	0.0263
313.15	0.9101	0.0268
313.15	1.0000	0.0277

Surface tension liquid-gas, N/m [ref]

Operational condition: Temperature, K = 293.15 (Liquid)

Mole fraction of Acetonitrile (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
0.1004	0.0240
0.2018	0.0242
0.3013	0.0245
0.5004	0.0253
0.7003	0.0265
0.8002	0.0273
0.8997	0.0282

Surface tension liquid-gas, N/m [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Acetonitrile (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
278.15	0.0000	0.0249
278.15	0.1255	0.0252
278.15	0.2452	0.0254
278.15	0.3466	0.0258
278.15	0.4995	0.0265
278.15	0.6449	0.0274
278.15	0.7492	0.0281
278.15	0.8645	0.0291
278.15	0.9101	0.0295
278.15	1.0000	0.0305
283.15	0.0000	0.0245
283.15	0.1255	0.0248
283.15	0.2452	0.0250
283.15	0.3466	0.0254
283.15	0.4995	0.0261
283.15	0.6449	0.0270
283.15	0.7492	0.0277
283.15	0.8645	0.0287
283.15	0.9101	0.0291
283.15	1.0000	0.0301
288.15	0.0000	0.0241
288.15	0.1255	0.0244
288.15	0.2452	0.0247
288.15	0.3466	0.0250
288.15	0.4995	0.0257
288.15	0.6449	0.0266
288.15	0.7492	0.0273
288.15	0.8645	0.0283
288.15	0.9101	0.0287
288.15	1.0000	0.0297
293.15	0.0000	0.0237
293.15	0.1255	0.0240
293.15	0.2452	0.0243
293.15	0.3466	0.0246
293.15	0.4995	0.0253
293.15	0.6449	0.0262
293.15	0.7492	0.0269
293.15	0.8645	0.0279
293.15	0.9101	0.0283
293.15	1.0000	0.0293
298.15	0.0000	0.0233
298.15	0.1255	0.0236
298.15	0.2452	0.0239
298.15	0.3466	0.0242
298.15	0.4995	0.0249
298.15	0.6449	0.0258
298.15	0.7492	0.0266
298.15	0.8645	0.0275
298.15	0.9101	0.0279
298.15	1.0000	0.0289
303.15	0.0000	0.0229
303.15	0.1255	0.0232
303.15	0.2452	0.0235
303.15	0.3466	0.0238
303.15	0.4995	0.0245
303.15	0.6449	0.0254
303.15	0.7492	0.0262
303.15	0.8645	0.0271
303.15	0.9101	0.0275
303.15	1.0000	0.0285
308.15	0.0000	0.0225
308.15	0.1255	0.0228
308.15	0.2452	0.0231
308.15	0.3466	0.0234
308.15	0.4995	0.0242
308.15	0.6449	0.0250
308.15	0.7492	0.0258
308.15	0.8645	0.0267
308.15	0.9101	0.0271
308.15	1.0000	0.0281
313.15	0.0000	0.0222
313.15	0.1255	0.0224
313.15	0.2452	0.0227
313.15	0.3466	0.0230
313.15	0.4995	0.0238
313.15	0.6449	0.0246
313.15	0.7492	0.0254
313.15	0.8645	0.0263
313.15	0.9101	0.0268
313.15	1.0000	0.0277

Surface tension liquid-gas, N/m [ref]

Operational condition: Temperature, K = 293.15 (Liquid)

Mole fraction of Acetonitrile (2) - Liquid	Surface tension liquid-gas, N/m - Liquid
0.1004	0.0240
0.2018	0.0242
0.3013	0.0245
0.5004	0.0253
0.7003	0.0265
0.8002	0.0273
0.8997	0.0282

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetonitrile (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0610	363.97
0.1110	361.37
0.1510	360.18
0.2080	359.05
0.2530	358.29
0.3490	356.63
0.4110	355.55
0.4650	354.72
0.5120	354.14
0.5700	353.67
0.6290	353.39
0.6900	353.21
0.7250	353.12
0.7800	352.91
0.8290	352.96
0.8830	353.17
0.9460	353.68
0.9790	354.06
0.9960	354.21

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetonitrile (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	370.33
0.0520	366.05
0.1030	362.92
0.1520	360.64
0.2050	358.93
0.2460	357.63
0.3010	356.61
0.3450	355.95
0.4020	355.25
0.4530	354.71
0.5010	354.34
0.5520	353.97
0.5890	353.66
0.6510	353.42
0.7030	353.21
0.7480	353.16
0.7980	353.18
0.8530	353.27
0.9020	353.47
0.9480	353.82
1.0000	354.74

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetonitrile (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0615	363.98
0.1121	361.38
0.1519	360.19
0.2086	359.06
0.2539	358.30
0.2910	357.68
0.3498	356.64
0.4115	355.56
0.4661	354.73
0.5132	354.15
0.5707	353.68
0.6300	353.40
0.6907	353.22
0.7235	353.13
0.7792	352.92
0.8283	352.97
0.8824	353.18
0.9451	353.69
0.9776	354.07
0.9953	354.22

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetonitrile (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0610	363.97
0.1110	361.37
0.1510	360.18
0.2080	359.05
0.2530	358.29
0.3490	356.63
0.4110	355.55
0.4650	354.72
0.5120	354.14
0.5700	353.67
0.6290	353.39
0.6900	353.21
0.7250	353.12
0.7800	352.91
0.8290	352.96
0.8830	353.17
0.9460	353.68
0.9790	354.06
0.9960	354.21

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetonitrile (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	370.33
0.0520	366.05
0.1030	362.92
0.1520	360.64
0.2050	358.93
0.2460	357.63
0.3010	356.61
0.3450	355.95
0.4020	355.25
0.4530	354.71
0.5010	354.34
0.5520	353.97
0.5890	353.66
0.6510	353.42
0.7030	353.21
0.7480	353.16
0.7980	353.18
0.8530	353.27
0.9020	353.47
0.9480	353.82
1.0000	354.74

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Acetonitrile (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0615	363.98
0.1121	361.38
0.1519	360.19
0.2086	359.06
0.2539	358.30
0.2910	357.68
0.3498	356.64
0.4115	355.56
0.4661	354.73
0.5132	354.15
0.5707	353.68
0.6300	353.40
0.6907	353.22
0.7235	353.13
0.7792	352.92
0.8283	352.97
0.8824	353.18
0.9451	353.69
0.9776	354.07
0.9953	354.22

Sources

• Application of the Extended Langmuir Model for the Determination of Lyophobicity of 1-Propanol in Acetonitrile
• (Vapour + liquid) equilibria in the ternary system (acetonitrile + n-propanol + ethylene glycol) and corresponding binary systems at 101.3 kPa
• Isobaric Vapor-Liquid Equilibrium of the Acetonitrile + 1-Propanol + Ionic Liquids at an Atmospheric Pressure
• Density and Surface Tension of Binary Mixtures of Acetonitrile + 1-Alkanol at 293.15 K
• Vapor-Liquid Equilibria for the Ternary System Acetonitrile + 1-Propanol + Dimethyl Sulfoxide and the Corresponding Binary Systems at 101.3 kPa